JPS6330215B2 - - Google Patents
Info
- Publication number
- JPS6330215B2 JPS6330215B2 JP57234864A JP23486482A JPS6330215B2 JP S6330215 B2 JPS6330215 B2 JP S6330215B2 JP 57234864 A JP57234864 A JP 57234864A JP 23486482 A JP23486482 A JP 23486482A JP S6330215 B2 JPS6330215 B2 JP S6330215B2
- Authority
- JP
- Japan
- Prior art keywords
- pet
- polyethylene terephthalate
- bottle
- vinyl acetate
- wax
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
- 239000000203 mixture Substances 0.000 claims description 39
- 229920000139 polyethylene terephthalate Polymers 0.000 claims description 28
- 239000005020 polyethylene terephthalate Substances 0.000 claims description 28
- 229920005989 resin Polymers 0.000 claims description 24
- 239000011347 resin Substances 0.000 claims description 24
- -1 polyethylene terephthalate Polymers 0.000 claims description 20
- 239000004831 Hot glue Substances 0.000 claims description 17
- 229920001200 poly(ethylene-vinyl acetate) Polymers 0.000 claims description 16
- 229920000642 polymer Polymers 0.000 claims description 15
- 239000001993 wax Substances 0.000 claims description 15
- 239000005038 ethylene vinyl acetate Substances 0.000 claims description 14
- 239000003921 oil Substances 0.000 claims description 12
- 239000003085 diluting agent Substances 0.000 claims description 11
- 239000003381 stabilizer Substances 0.000 claims description 11
- KAKZBPTYRLMSJV-UHFFFAOYSA-N Butadiene Chemical compound C=CC=C KAKZBPTYRLMSJV-UHFFFAOYSA-N 0.000 claims description 8
- 229920001400 block copolymer Polymers 0.000 claims description 8
- 229920001577 copolymer Polymers 0.000 claims description 8
- 238000002844 melting Methods 0.000 claims description 7
- 230000008018 melting Effects 0.000 claims description 7
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 claims description 5
- XTXRWKRVRITETP-UHFFFAOYSA-N Vinyl acetate Chemical compound CC(=O)OC=C XTXRWKRVRITETP-UHFFFAOYSA-N 0.000 claims description 5
- 150000001993 dienes Chemical class 0.000 claims description 5
- 239000000155 melt Substances 0.000 claims description 5
- 239000004793 Polystyrene Substances 0.000 claims description 4
- 150000004945 aromatic hydrocarbons Chemical class 0.000 claims description 4
- 150000005673 monoalkenes Chemical class 0.000 claims description 4
- 239000003208 petroleum Substances 0.000 claims description 4
- 229920002223 polystyrene Polymers 0.000 claims description 4
- 239000007787 solid Substances 0.000 claims description 4
- 235000007586 terpenes Nutrition 0.000 claims description 4
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 claims description 3
- 241001465754 Metazoa Species 0.000 claims description 3
- 239000004698 Polyethylene Substances 0.000 claims description 3
- 229920001971 elastomer Polymers 0.000 claims description 3
- 229920001903 high density polyethylene Polymers 0.000 claims description 3
- 239000004700 high-density polyethylene Substances 0.000 claims description 3
- 239000002480 mineral oil Substances 0.000 claims description 3
- 235000010446 mineral oil Nutrition 0.000 claims description 3
- 229920000573 polyethylene Polymers 0.000 claims description 3
- 150000003097 polyterpenes Chemical class 0.000 claims description 3
- 229920000468 styrene butadiene styrene block copolymer Polymers 0.000 claims description 3
- 241000251468 Actinopterygii Species 0.000 claims description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 2
- 239000013032 Hydrocarbon resin Substances 0.000 claims description 2
- 239000004743 Polypropylene Substances 0.000 claims description 2
- 125000001931 aliphatic group Chemical group 0.000 claims description 2
- 229910002091 carbon monoxide Inorganic materials 0.000 claims description 2
- 235000011187 glycerol Nutrition 0.000 claims description 2
- 229920006270 hydrocarbon resin Polymers 0.000 claims description 2
- 229910052739 hydrogen Inorganic materials 0.000 claims description 2
- 239000001257 hydrogen Substances 0.000 claims description 2
- 238000006116 polymerization reaction Methods 0.000 claims description 2
- 229920001155 polypropylene Polymers 0.000 claims description 2
- 150000003505 terpenes Chemical class 0.000 claims description 2
- 241000196324 Embryophyta Species 0.000 claims 1
- 125000004435 hydrogen atom Chemical class [H]* 0.000 claims 1
- 239000004200 microcrystalline wax Substances 0.000 claims 1
- 235000019808 microcrystalline wax Nutrition 0.000 claims 1
- 235000014593 oils and fats Nutrition 0.000 claims 1
- WXZMFSXDPGVJKK-UHFFFAOYSA-N pentaerythritol Chemical class OCC(CO)(CO)CO WXZMFSXDPGVJKK-UHFFFAOYSA-N 0.000 claims 1
- 229920006132 styrene block copolymer Polymers 0.000 claims 1
- 239000000853 adhesive Substances 0.000 description 23
- 230000001070 adhesive effect Effects 0.000 description 23
- RSWGJHLUYNHPMX-UHFFFAOYSA-N Abietic-Saeure Natural products C12CCC(C(C)C)=CC2=CCC2C1(C)CCCC2(C)C(O)=O RSWGJHLUYNHPMX-UHFFFAOYSA-N 0.000 description 12
- KHPCPRHQVVSZAH-HUOMCSJISA-N Rosin Natural products O(C/C=C/c1ccccc1)[C@H]1[C@H](O)[C@@H](O)[C@@H](O)[C@@H](CO)O1 KHPCPRHQVVSZAH-HUOMCSJISA-N 0.000 description 12
- KHPCPRHQVVSZAH-UHFFFAOYSA-N trans-cinnamyl beta-D-glucopyranoside Natural products OC1C(O)C(O)C(CO)OC1OCC=CC1=CC=CC=C1 KHPCPRHQVVSZAH-UHFFFAOYSA-N 0.000 description 12
- 235000019198 oils Nutrition 0.000 description 9
- 229920003345 Elvax® Polymers 0.000 description 8
- 239000000178 monomer Substances 0.000 description 8
- 150000002989 phenols Chemical class 0.000 description 7
- 229920002633 Kraton (polymer) Polymers 0.000 description 6
- 238000000034 method Methods 0.000 description 6
- 238000002156 mixing Methods 0.000 description 4
- 239000003784 tall oil Substances 0.000 description 4
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 239000012188 paraffin wax Substances 0.000 description 3
- 238000003756 stirring Methods 0.000 description 3
- VSKJLJHPAFKHBX-UHFFFAOYSA-N 2-methylbuta-1,3-diene;styrene Chemical compound CC(=C)C=C.C=CC1=CC=CC=C1.C=CC1=CC=CC=C1 VSKJLJHPAFKHBX-UHFFFAOYSA-N 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- RRHGJUQNOFWUDK-UHFFFAOYSA-N Isoprene Chemical compound CC(=C)C=C RRHGJUQNOFWUDK-UHFFFAOYSA-N 0.000 description 2
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 2
- 239000007983 Tris buffer Substances 0.000 description 2
- 239000000654 additive Substances 0.000 description 2
- FACXGONDLDSNOE-UHFFFAOYSA-N buta-1,3-diene;styrene Chemical compound C=CC=C.C=CC1=CC=CC=C1.C=CC1=CC=CC=C1 FACXGONDLDSNOE-UHFFFAOYSA-N 0.000 description 2
- 239000012943 hotmelt Substances 0.000 description 2
- 229930195733 hydrocarbon Natural products 0.000 description 2
- 238000010525 oxidative degradation reaction Methods 0.000 description 2
- CMPQUABWPXYYSH-UHFFFAOYSA-N phenyl phosphate Chemical compound OP(O)(=O)OC1=CC=CC=C1 CMPQUABWPXYYSH-UHFFFAOYSA-N 0.000 description 2
- 230000000379 polymerizing effect Effects 0.000 description 2
- 235000014214 soft drink Nutrition 0.000 description 2
- 238000003860 storage Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 125000001424 substituent group Chemical group 0.000 description 2
- 229910052717 sulfur Inorganic materials 0.000 description 2
- 239000011593 sulfur Substances 0.000 description 2
- LENZDBCJOHFCAS-UHFFFAOYSA-N tris Chemical group OCC(N)(CO)CO LENZDBCJOHFCAS-UHFFFAOYSA-N 0.000 description 2
- TUYBEVLJKZQJPO-UHFFFAOYSA-N 19-(3,5-ditert-butyl-4-hydroxyphenyl)heptatriacontan-19-ylphosphonic acid Chemical compound CCCCCCCCCCCCCCCCCCC(CCCCCCCCCCCCCCCCCC)(P(O)(O)=O)C1=CC(C(C)(C)C)=C(O)C(C(C)(C)C)=C1 TUYBEVLJKZQJPO-UHFFFAOYSA-N 0.000 description 1
- KGRVJHAUYBGFFP-UHFFFAOYSA-N 2,2'-Methylenebis(4-methyl-6-tert-butylphenol) Chemical compound CC(C)(C)C1=CC(C)=CC(CC=2C(=C(C=C(C)C=2)C(C)(C)C)O)=C1O KGRVJHAUYBGFFP-UHFFFAOYSA-N 0.000 description 1
- DKCPKDPYUFEZCP-UHFFFAOYSA-N 2,6-di-tert-butylphenol Chemical compound CC(C)(C)C1=CC=CC(C(C)(C)C)=C1O DKCPKDPYUFEZCP-UHFFFAOYSA-N 0.000 description 1
- JQTAVKOFIFYMKC-UHFFFAOYSA-N 2-octylsulfanylethyl 3,5-ditert-butyl-4-hydroxybenzoate Chemical compound CCCCCCCCSCCOC(=O)C1=CC(C(C)(C)C)=C(O)C(C(C)(C)C)=C1 JQTAVKOFIFYMKC-UHFFFAOYSA-N 0.000 description 1
- YFHKLSPMRRWLKI-UHFFFAOYSA-N 2-tert-butyl-4-(3-tert-butyl-4-hydroxy-5-methylphenyl)sulfanyl-6-methylphenol Chemical compound CC(C)(C)C1=C(O)C(C)=CC(SC=2C=C(C(O)=C(C)C=2)C(C)(C)C)=C1 YFHKLSPMRRWLKI-UHFFFAOYSA-N 0.000 description 1
- WPMYUUITDBHVQZ-UHFFFAOYSA-M 3-(3,5-ditert-butyl-4-hydroxyphenyl)propanoate Chemical compound CC(C)(C)C1=CC(CCC([O-])=O)=CC(C(C)(C)C)=C1O WPMYUUITDBHVQZ-UHFFFAOYSA-M 0.000 description 1
- MDWVSAYEQPLWMX-UHFFFAOYSA-N 4,4'-Methylenebis(2,6-di-tert-butylphenol) Chemical compound CC(C)(C)C1=C(O)C(C(C)(C)C)=CC(CC=2C=C(C(O)=C(C=2)C(C)(C)C)C(C)(C)C)=C1 MDWVSAYEQPLWMX-UHFFFAOYSA-N 0.000 description 1
- VSAWBBYYMBQKIK-UHFFFAOYSA-N 4-[[3,5-bis[(3,5-ditert-butyl-4-hydroxyphenyl)methyl]-2,4,6-trimethylphenyl]methyl]-2,6-ditert-butylphenol Chemical compound CC1=C(CC=2C=C(C(O)=C(C=2)C(C)(C)C)C(C)(C)C)C(C)=C(CC=2C=C(C(O)=C(C=2)C(C)(C)C)C(C)(C)C)C(C)=C1CC1=CC(C(C)(C)C)=C(O)C(C(C)(C)C)=C1 VSAWBBYYMBQKIK-UHFFFAOYSA-N 0.000 description 1
- RSFMBVKVSSHYLS-UHFFFAOYSA-N 4-[[4,6-bis(3,5-ditert-butyl-4-hydroxyphenoxy)-1,3,5-triazin-2-yl]oxy]-2,6-ditert-butylphenol Chemical compound CC(C)(C)C1=C(O)C(C(C)(C)C)=CC(OC=2N=C(OC=3C=C(C(O)=C(C=3)C(C)(C)C)C(C)(C)C)N=C(OC=3C=C(C(O)=C(C=3)C(C)(C)C)C(C)(C)C)N=2)=C1 RSFMBVKVSSHYLS-UHFFFAOYSA-N 0.000 description 1
- XPOLRBKMCIXLQT-UHFFFAOYSA-N 4-[[4,6-bis(octylsulfanyl)-1,3,5-triazin-2-yl]oxy]phenol Chemical compound CCCCCCCCSC1=NC(SCCCCCCCC)=NC(OC=2C=CC(O)=CC=2)=N1 XPOLRBKMCIXLQT-UHFFFAOYSA-N 0.000 description 1
- 239000004322 Butylated hydroxytoluene Substances 0.000 description 1
- NLZUEZXRPGMBCV-UHFFFAOYSA-N Butylhydroxytoluene Chemical compound CC1=CC(C(C)(C)C)=C(O)C(C(C)(C)C)=C1 NLZUEZXRPGMBCV-UHFFFAOYSA-N 0.000 description 1
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- FBPFZTCFMRRESA-FSIIMWSLSA-N D-Glucitol Natural products OC[C@H](O)[C@H](O)[C@@H](O)[C@H](O)CO FBPFZTCFMRRESA-FSIIMWSLSA-N 0.000 description 1
- 238000005727 Friedel-Crafts reaction Methods 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- 229920013623 Solprene Polymers 0.000 description 1
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 238000004026 adhesive bonding Methods 0.000 description 1
- 150000001336 alkenes Chemical class 0.000 description 1
- 239000012164 animal wax Substances 0.000 description 1
- 230000000712 assembly Effects 0.000 description 1
- 238000000429 assembly Methods 0.000 description 1
- 229930003642 bicyclic monoterpene Natural products 0.000 description 1
- 150000001604 bicyclic monoterpene derivatives Chemical class 0.000 description 1
- 229940095259 butylated hydroxytoluene Drugs 0.000 description 1
- 235000010354 butylated hydroxytoluene Nutrition 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000004359 castor oil Substances 0.000 description 1
- 235000019438 castor oil Nutrition 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 239000002738 chelating agent Substances 0.000 description 1
- 239000004927 clay Substances 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 235000012716 cod liver oil Nutrition 0.000 description 1
- 239000003026 cod liver oil Substances 0.000 description 1
- 235000012343 cottonseed oil Nutrition 0.000 description 1
- 239000002385 cottonseed oil Substances 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 230000000593 degrading effect Effects 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 229910000071 diazene Inorganic materials 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- ZEMPKEQAKRGZGQ-XOQCFJPHSA-N glycerol triricinoleate Natural products CCCCCC[C@@H](O)CC=CCCCCCCCC(=O)OC[C@@H](COC(=O)CCCCCCCC=CC[C@@H](O)CCCCCC)OC(=O)CCCCCCCC=CC[C@H](O)CCCCCC ZEMPKEQAKRGZGQ-XOQCFJPHSA-N 0.000 description 1
- 238000007757 hot melt coating Methods 0.000 description 1
- 150000004678 hydrides Chemical class 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 238000005984 hydrogenation reaction Methods 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 238000005304 joining Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- ABCGFHPGHXSVKI-UHFFFAOYSA-O meso-tetrakis(n-methyl-4-pyridyl)porphine(4+) Chemical compound C1=C[N+](C)=CC=C1C(C1=CC=C(N1)C(C=1C=C[N+](C)=CC=1)=C1C=CC(=N1)C(C=1C=C[N+](C)=CC=1)=C1C=CC(N1)=C1C=2C=C[N+](C)=CC=2)=C2N=C1C=C2 ABCGFHPGHXSVKI-UHFFFAOYSA-O 0.000 description 1
- 239000006078 metal deactivator Substances 0.000 description 1
- SSDSCDGVMJFTEQ-UHFFFAOYSA-N octadecyl 3-(3,5-ditert-butyl-4-hydroxyphenyl)propanoate Chemical compound CCCCCCCCCCCCCCCCCCOC(=O)CCC1=CC(C(C)(C)C)=C(O)C(C(C)(C)C)=C1 SSDSCDGVMJFTEQ-UHFFFAOYSA-N 0.000 description 1
- AQSJGOWTSHOLKH-UHFFFAOYSA-N phosphite(3-) Chemical class [O-]P([O-])[O-] AQSJGOWTSHOLKH-UHFFFAOYSA-N 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 239000000049 pigment Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920000728 polyester Polymers 0.000 description 1
- 235000015277 pork Nutrition 0.000 description 1
- 239000010734 process oil Substances 0.000 description 1
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 1
- 230000009257 reactivity Effects 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000000600 sorbitol Substances 0.000 description 1
- 235000012424 soybean oil Nutrition 0.000 description 1
- 239000003549 soybean oil Substances 0.000 description 1
- 230000000087 stabilizing effect Effects 0.000 description 1
- 125000003011 styrenyl group Chemical group [H]\C(*)=C(/[H])C1=C([H])C([H])=C([H])C([H])=C1[H] 0.000 description 1
- 239000000454 talc Substances 0.000 description 1
- 229910052623 talc Inorganic materials 0.000 description 1
- 239000003760 tallow Substances 0.000 description 1
- 125000000999 tert-butyl group Chemical group [H]C([H])([H])C(*)(C([H])([H])[H])C([H])([H])[H] 0.000 description 1
- 238000010998 test method Methods 0.000 description 1
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 description 1
- 229920000428 triblock copolymer Polymers 0.000 description 1
- WGKLOLBTFWFKOD-UHFFFAOYSA-N tris(2-nonylphenyl) phosphite Chemical compound CCCCCCCCCC1=CC=CC=C1OP(OC=1C(=CC=CC=1)CCCCCCCCC)OC1=CC=CC=C1CCCCCCCCC WGKLOLBTFWFKOD-UHFFFAOYSA-N 0.000 description 1
- MGMXGCZJYUCMGY-UHFFFAOYSA-N tris(4-nonylphenyl) phosphite Chemical compound C1=CC(CCCCCCCCC)=CC=C1OP(OC=1C=CC(CCCCCCCCC)=CC=1)OC1=CC=C(CCCCCCCCC)C=C1 MGMXGCZJYUCMGY-UHFFFAOYSA-N 0.000 description 1
- 235000015112 vegetable and seed oil Nutrition 0.000 description 1
- 239000008158 vegetable oil Substances 0.000 description 1
- 239000012178 vegetable wax Substances 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09J—ADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
- C09J191/00—Adhesives based on oils, fats or waxes; Adhesives based on derivatives thereof
- C09J191/06—Waxes
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09J—ADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
- C09J153/00—Adhesives based on block copolymers containing at least one sequence of a polymer obtained by reactions only involving carbon-to-carbon unsaturated bonds; Adhesives based on derivatives of such polymers
- C09J153/02—Vinyl aromatic monomers and conjugated dienes
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L2666/00—Composition of polymers characterized by a further compound in the blend, being organic macromolecular compounds, natural resins, waxes or and bituminous materials, non-macromolecular organic substances, inorganic substances or characterized by their function in the composition
- C08L2666/02—Organic macromolecular compounds, natural resins, waxes or and bituminous materials
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/13—Hollow or container type article [e.g., tube, vase, etc.]
- Y10T428/1352—Polymer or resin containing [i.e., natural or synthetic]
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/13—Hollow or container type article [e.g., tube, vase, etc.]
- Y10T428/1352—Polymer or resin containing [i.e., natural or synthetic]
- Y10T428/1386—Natural or synthetic rubber or rubber-like compound containing
Description
発明の分野
本発明は、ポリエチレン製の底ぶたが新規なホ
ツトメルト接着剤組成物によつてブロー成形ポリ
エチレンテレフタレート(PET)びんに接合さ
れている組立てびん(bottle assembly)に関す
るものである。さらに詳しくは、本発明は底ぶた
をPETびんに接合、組み立てる際に特に有用な
改良された性質を有する新規なホツトメルト接着
剤組成物に関する。
先行技術の簡単な説明
ポリエステル製のびんは清涼飲料工業で広く用
いられている。これらのびんは通常ブロー成形で
造られた丸底のびんで、真直ぐに立てるために別
の底ぶたを必要とする。この底ぶたはびんを、び
ん詰め条件、取扱い条件及び貯蔵条件に耐えて十
分元の状態に保たせる役目を持つ。この底ぶたは
通常高密度ポリエチレン(HDPE)で作られてお
り、ホツトメルト接着剤によりびんに接合されて
いる。
組立てびんがびん詰め、取扱い及び貯蔵中に受
ける力は、底ぶたをびんに保持している接着結合
をかなりの応力下に置き、それによつて底ぶたと
組立びんが剥れたり、離れたりする原因となる。
このような応力は充てん前に空びんをはく離さ
せる原因となるので、このようなびんは自動充て
んラインに使用できない。びんが充てんされる
と、内容物による圧力でびんと底ぶたの間の機械
的な適合性が改善され、底ぶたはびんに接合した
状態に保持されるようになる。しかし、内容物の
一部でも無くなると、この改善された適合性が失
われるので、接着剤はびんと底ぶたが離れるのを
防がなければならない。また接着剤は温度及び湿
度条件の変動によつて充てんの前及び後で組立て
びんが受ける応力に耐えなければならない。
清涼飲料充てん工業では、組立てびんが満さな
ければならない一連の規格を作つている。たとえ
ば、組立てびんは、空の場合−17.8℃(0〓)に
冷却し、1.83m(6フイート)の高さから落した
時、また充てんされている場合は4.5℃(40〓)
で1.83メートルの高さから落した時に離れてはい
けない。
テイラー(Taylor)達は米国特許第4212910号
明細書(特開昭55−154235号公報に相当)におい
て、接着剤組成物がスチレン−ブタジエン−スチ
レン型またはスチレン−イソプレン−スチレン型
ブロツク共重合体、粘着付与樹脂、安定剤および
ワツクスまたは油性希釈剤から成る混合物である
組立てびんについて述べ、かつ特許請求してい
る。この組成物は以前に用いられていた接着剤よ
りは改善されているが、難点がないわけではな
い。たとえば、室温における接着剤組成物の結合
強さは要求される値より低く、組成物の温度安定
性は改善の余地を残している。
本発明の要約
本発明の一般的目的は、PET製のびんと底ぶ
たとの間の接着結合がその組立てびんが受けると
考えられる全ての通常の応力に耐えるところの
PET組立てびんを製造することである。
さらに本発明のもう一つの目的は、PET組立
てびんに使用した場合びん詰め工業で要求される
規格を満す接着結合を生成させる接着剤組成物を
提供することである。
本発明で用いられる接着剤組成物は次の(1)から
(5)の成分の混合物である:(1)Aがモノビニル芳香
族炭化水素で、Bが共役ジエンまたはゴム系モノ
オレフインであるA−B−A型ブロツク共重合体
(a)及び中心セグメントから放射状に枝分れした少
なくとも三つの枝を持ち、その各枝がポリスチレ
ンの末端ブロツクとブタジエンの中心セグメント
を持つ分子から成るテレブロツク共重合体(b);(2)
エチレン−酢酸ビニル共重合体;(3)混合物系の接
着性を大きくするのに役立つ少なくとも一種の粘
着付与樹脂;(4)少なくとも一種の安定剤、及び(5)
少くとも一種のワツクスまたは油系希釈剤。
本発明で用いられる接着剤組成物は基本成分の
一つとしてエチレン−酢酸ビニル共重合体を含ん
でいる点でテイラー(Taylor)達の米国特許第
4212910号の接着剤組成物と著しく異なつている。
本発明者は、テイラー達の特許に記載された接
着剤組成物にエチレン−酢酸ビニル共重合体を添
加すると、テイラー達の組成物の全ての利点に加
えて価格が下り、室温でも接着強さが改善され、
さらに高温での安定性が向上することを発見し
た。エチレン−酢酸ビニル共重合体を添加する
と、このような利点が得られるという発見は驚く
べきことである。何故なら、テイラー達の特許明
細書には、既知のエチレン−酢酸ビニル共重合体
(EVA)を基体とするホツトメルト接着剤を用い
ると、PET組立てびんの場合びん詰め工業の規
格を充たすことはできないと述べられているから
である(該特許明細書コラム1の52〜56行及びコ
ラム6の6〜32行)。テイラー達の特許明細書は、
当該技術での習熟者に対し、テイラー達の接着剤
組成物にエチレン−酢酸ビニル共重合体を添加す
るとこれら組成物に何らかの改善が見られるとい
うことを示唆していないことは明らかである。
本発明の接着剤組成物を用いて作られた組立て
びんは低温、常温及び高温での素晴らしい接着性
と柔軟性、さらに高い結合強さを兼ね備えた結合
を有している。
好ましい実施態様の説明
本発明で用いられるホツトメルト接着剤のブロ
ツク共重合体成分(1)は、次の二つの特定の組の内
の一つでよい。
(a) それぞれの単量体部分がA−B−Aの一般構
造を持つように交互に配列しており、Aはモノ
ビニル芳香族炭化水素系単量体部分から成る非
弾性ブロツクであり、Bは共役ジエン単量体ま
たはモノ−オレフインのいずれかの部分から成
る弾性重合体ブロツクであり、Aブロツクの全
濃度が該重合体の全重量の約10〜50%の範囲で
あるような未加硫弾性ブロツク重合体。これら
重合体の中で、モノビニル芳香族炭化水素単量
体として通常用いられるのはスチレンである。
また共役ジエン単量体として最もよく用いられ
るのはブタジエン−1,3とイソプレンであ
る。かくして、たとえばスチレン−ブタジエン
−スチレン重合体はシエル・ケミカル・カンパ
ニー(Shell Chemical Co.)から“クレイト
ン1101”及び“クレイトン1102”(Kraton−
1101、−1102)という商標で市販されており、
またスチレン−イソプレン−スチレン重合体は
“クレイトン1107”及び“クレイトン84−0554”
という商標で市販されている。またモノオレフ
インとして通常用いられるのはエチレンブチレ
ン単量体であるが、その他の単量体成分も用い
られる。使用に適したスチレン−エチレンブチ
レン−スチレン共重合体がシエルケミカルカン
パニーから“クレイトンG”という商標で市販
されている。本発明の組成物に使用するのに望
ましいブロツク共重合体はクレイトン1102であ
る。
(b) 中心セグメントから放射状に枝分れした少な
くとも三つの枝を持ち、その各枝がポリスチレ
ンの末端ブロツクとブタジエンの中心セグメン
トを持つ分子から成るテレブロツク共重合体。
このタイプのブロツク共重合体は各枝の末端に
ポリスチレン末端ブロツクを有する分枝、重合
したブタジエン中心ブロツクと称することもで
きる。全ての場合、ブタジエン単位の数はスチ
レン単位の数より多くなければならない。代表
的テレブロツク共重合体がソルプレン
(SOLPRENE)という商標で、フイリツプス
ペトロリアムカンパニー(Phillips Petroleum
Company)から市販されている。
上記ブロツク共重合体の任意の物の混合物もま
た本発明のPET組立てびんに用いられる接着剤
の基本成分として当然使用できる。
本発明で用いられるホツトメルト接着剤のエチ
レン−酢酸ビニル共重合体成分(2)は、当該技術分
野で特にホツトメルト被覆材及び接着剤中の混合
用樹脂としてよく知られている。
製造会社数社がこの共重合体を製造している。
デユポン社(Du Pont)のプラスチツク製品及び
樹脂部門では“エルバツクス”(“Elvax”)と
いう一般商標で組成と粘度の組合せの異なる多数
の製品を製造している。エルバツクス樹脂は酢酸
ビニル含有量によつて“グレード”に分類して売
られている。たとえば、200−シリーズの樹脂は
約28パーセントの酢酸ビニルを含み、300−シリ
ーズは25パーセント、そして400−シリーズは18
パーセントの酢酸ビニルを含む。これら各シリー
ズの中で、グレード番号が大きくなると固有粘度
が増す。たとえば、エルバツクス210の固有粘度
は0.54、エルバツクス260は0.94、エルバツクス
265は1.01である。これらの樹脂の中で、メルト
インデツクス400のエルバツクス210が本発明の組
成物に用いた場合特に効果的である。全てのグレ
ードのエルバツクスは50〜1000ppmのブチル化ヒ
ドロキシトルエンを添加して安定化され、使用時
の粘度変化を防いでいる。
本発明のホツトメルト接着剤に用いられている
粘着付与樹脂(3)は該ブロツク重合体の接着性を増
大させると考えられる。ここで用いられる“粘着
付与樹脂”という用語は次の(a)〜(e)の樹脂を意味
する。すなわち、(a)ゴムロジン、木材ロジン、ト
ール油ロジン、蒸留ロジン、水素化ロジン、二量
化ロジン及び重合ロジンのような天然及び変性ロ
ジン;(b)たとえば、ペールウツドロジンのグリセ
リンエステル、水素化ロジンのグリセリンエステ
ル、重合ロジンのグリセリンエステル、水素化ロ
ジンのペンタエリトリトールエステル及びロジン
のフエノール変性ペンタエリトリトールエステル
などのような天然及び変性ロジンのグリセリン及
びペンタエリトリトールエステル類;(c)ASTM
法E2858Tで測定した軟化点が約60から140℃であ
るポリテルペン樹脂。この内高軟化点のポリテル
ペン樹脂は通常比較的低温でフリーデル−クラフ
ツ触媒の存在下でピネンとして知られている二環
状モノテルペンのようなテルペン炭化水素を重合
することにより得られる;(d)たとえば、二環状テ
ルペン及びフエノールを酸性媒体中で縮合させて
得られる樹脂生成物のようなフエノール変性テル
ペン樹脂;及び(e)環球式軟化点が約60から140℃
である脂肪族石油系炭化水素樹脂、この内高軟化
点の樹脂は主としてオレフイン及びジオレフイン
から成る単量体の重合により得られる。特に推奨
される物はシルバヘム コーポレーシヨン オブ
ジヤクソンビル(Sylvachem Corpration of
Jacksonville)、フロリダ(FFlorida)からシル
バタツク95(SYLVATAC95)の名前で売られて
いる重合トール油ロジンである。
本発明のホツトメルト接着剤組成物中に用いら
れる安定剤(4)は或る意味では侵され易いブロツク
重合体を、従つて全接着剤系を、その接着剤の製
造及び使用中にさらに最終接着製品が通常曝され
る条件でよく遭遇する熱及び酸化分解から防ぐの
に役立つ。エチレン−酢酸ビニル共重合体もブロ
ツク重合体を熱及び酸化分解から防ぐのに役立つ
と考えられる。かゝる分解は通常、外観、物理的
性質及び実用性能の悪化に現れて来る。用いられ
る安定剤には分子量の大きい立体的にひずんだフ
エノール及び硫黄やりんを含むフエノール類のよ
うな多官能性フエノール類が含まれる。ヒンダー
ドフエノールは当該技術分野での専門家にはよく
知られており、そのフエノール性水酸基のすぐ近
くに立体的にかさ高い基を持つことが特徴のフエ
ノール系化合物である。特に、フエノール性水酸
基のオルソ位の少なくとも一つに第三ブチル基が
通常置換基として含まれている。このような立体
的にかさ高い置換基が水酸基の近くに存在する
と、その伸縮振動、従つてその反応性が抑制され
る。かくて、この立体障害が安定化性能を持つた
フエノール系化合物を提供することになる。代表
的ヒンダードフエノールは1,3,5−トリメチ
ル−2,4,6−トリス(3,5−ジ第三ブチル
−4−ヒドロキシベンジル)ベンゼン、ペンタエ
リトリチルテトラキス−3(3,5−ジ第三ブチ
ル−4−ヒドロキシフエニル)プロピオネート、
n−オクタデシル−3(3,5−ジ第三ブチル−
4−ヒドロキシフエニル)プロピオネート;4,
4′−メチレン−ビス(2,6−ジ第三ブチルフエ
ノール);2,2′−メチレンビス(4−メチル−
6−第三ブチルフエノール);4,4′−チオビス
(6−第三ブチル−o−クレゾール);2,6−ジ
第三ブチルフエノール);6−(4−ヒドロキシフ
エノキシ)−2,4−ビス(n−オクチルチオ)−
1,3,5−トリアジン;2,4,6−トリス
(4−ヒドロキシ−3,5−ジ第三ブチルフエノ
キシ)−1,3,5−トリアジン;ジ−n−オク
タデシル−3,5−ジ−第三ブチル−4−ヒドロ
キシベンジルホスホネート;2−(n−オクチル
チオ)エチル−3,5−ジ第三ブチル−4−ヒド
ロキシベンゾエート;及びソルビトールヘキサ
〔3−(3,5−ジ第三ブチル−4−ヒドロキシフ
エニル)プロピオネート〕である。安定剤として
特に推奨される物はウエストン社(Weston)か
らTNPPという商品名で市販されているトリス
(モノフエニルホスフエート)である。
これら安定剤の性能は次の(1)及び(2)を併用する
とさらに向上する:(1)たとえばチオジプロピオン
酸エステル及び亜リン酸エステルのような相乗
剤、及び(2)たとえば、エチレンジアミン四酢酸、
その塩、及びジサリシラルプロピレンジイミンの
ようなキレート剤および金属奪活剤。
本発明で用いられるワツクスまたは油系希釈剤
(5)はホツトメルト接着剤組成物の溶融粘度または
凝集性をその接着結合特性を認められる程悪化さ
せることなく、低下させる。用いられるワツクス
系希釈剤には次のものが含まれる:
(1)ASTM法D−1321で測定した硬度が約0.1〜
120で、ASTM軟化点が約65.6〜121℃(150〜
250〓)である分子量の低い、たとえば1000〜
6000のポリエチレン、(2)融点約54.5〜79.5℃
(130〜175〓)のパラフインワツクス及びASTM
法D127−60で測定した融点が約57.2〜93.3℃
(135〜200〓)の微細結晶性ワツクス;(3)環球式
軟化点が約120〜160℃のアタクチツクポリプロピ
レン、及び(4)フイツシヤートロプツシユ・ワツク
ス(Fischer−Tropsch Wax)のような一酸化炭
素と水素との重合で造られた合成ワツクス。これ
らワツクス系希釈剤はいずれも室温では固体であ
る。水素化獣脂、豚油、大豆油、棉実油、ひまし
油、メンヘーデイン油、肝油などのような水素化
動物、魚及び植物油脂類は水素化により常温で固
体になつているのでワツクス系希釈剤と同等な物
として有用なことが分つた。これらの水素化物は
接着剤工業ではしばしば“動物または植物ワツク
ス”と呼ばれている。さらに炭化水素油、特にナ
フテンまたはパラフイン・プロセス油も本発明の
希釈剤として用いられる。特に、融点150℃のパ
ラフインワツクスと白色鉱油(white mineral
oil)U.S.P.とを併用するのがよい。
本発明の新規ホツトメルト接着剤組成物の代表
的な物は濃度約20〜40%のブロツク重合体、濃度
約5〜20%のエチレン−酢酸ビニル共重合体、濃
度約30〜60%の粘着付与樹脂、濃度約0.1〜4%
の安定剤及び濃度約10〜30%のワツクスまたは油
を含んでいる。そしてこれらの濃度は該ホツトメ
ルト接着剤組成物の固体全重量を100%として計
算した値である。
本発明で用いられるホツトメルト接着剤組成物
は当該技術分野で知られている任意の技術を用い
て調合される。代表的方法は以下の通りである:
ジヤケツトの付いた混合装置、望ましくはかくは
ん機を備えたベイカー・パーキンス型(Baker−
Perkins)またはデイ(Day)型のジヤケツト付
きの丈夫な混合機中に粘着付与樹脂の約半量、ワ
ツクスと油及び安定剤の全量を入れ、すぐに温度
を約121〜176.7℃(250〜350〓)、望ましくは149
℃(300〓)に上げる。用いられる正確な温度は
特定の成分に融点に依存する。この出発混合物が
融けて混合されてからCO2をゆつくり通して混合
物を覆つてからブロツク重合体を加える。このブ
ロツク重合体が溶けてからエチレン−酢酸ビニル
共重合体を加え、なめらかになるまで混合する。
次いで残りの粘結付与樹脂を加え、良く混ざるま
で混合を続ける。
該ホツトメルト組成物の粘度は162.8℃(325
〓)で約4000センチポイズであることが望まし
い。
該ホツトメルト組成物の性質を改良するため
に、任意の添加剤を加えてもよい。これら添加剤
の中には、酸化チタンなどの顔料、タルクや粘土
のような充てん剤などが含まれる。
本発明のPET組立てびんは、通常びんと底ぶ
たを直線型または遠心型のフイーダー上に供給
し、多孔ノズルからホツトメルト接着剤を小滴状
にして底ぶた当たり約0.4〜0.75gの塗布量にな
るように塗布し、次いでびんと底ぶたとを少なく
とも6.5秒挾み合せて、小滴状のホツトメルト接
着剤がつながつて線状になり、適当にセツトされ
るようにする方法で製造される。次いで、この組
立てびんにラベルを付け、包装して、びん詰め作
業のために出荷するパレツトに乗せられる。
以下の参考例及び実施例により本発明の実施態
様をさらに具体的に説明する。
参考例
かくはん用の櫂状の羽根を備えた丈夫なかま型
混合機を149℃(300〓)に加熱し、融点65.6℃
(150〓)のパラフイン・ワツクス373.8Kg(824ポ
ンド)、白色鉱油U.S.P.249Kg(549ポンド)、トリ
スモノフエノール・ホスフエート(ウエストン
TNPP)(Weston TMPP)3.6Kg((8ポンド)
及び重合トール油ロジン(シルバタツク95
(Sylvatac95)488.5Kg(1077ポンド)を仕込ん
だ。この混合物を溶融し、混ぜ合せ、炭酸ガスを
ゆつくり封入した後“クレイトン1102”の商標で
シエルケミカルカンパニーから市販されているブ
ロツク重合体622.8Kg(1373ポンド)を加えた。
このブロツク重合体が溶けてからメルトインデツ
クス400のエチレン−酢酸ビニル共重合体(エル
バツクス210)249Kg(549ポンド)をかき混げな
がら加えた。この混合物がなめらかになつてから
重合トール油ロジン(シルバタツク95)508Kg
(1120ポンド)を加えた。かくはんを遅くした時、
全体が均質で十分混合された塊状になるまで混合
を続ける。この融解混合物を仕切られた容器に流
し込んで固める。このようにして得られた製品は
ブルツクフイールドサーモセル(スピンドル
#27、20回転/分)を備えたブルツク・フイール
ド回転粘度計で測定した溶融粘度が162.8℃(325
〓)で約4000センチポイズであつた。
実施例
前記参考例で調製したホツトメルト接着剤組成
物を用い、在来の製造装置を用いてPET組立て
びんを造つた。この組立てびんをびん詰め工業で
定められた各種試験法で試験し、これら規格を満
すか、またはそれ以上の性能を持つことを示し
た。
比較のために、本発明の組成物とエチレン−酢
酸ビニル共重合体を含んでいない点を除いて本発
明の組成物と同一である接着剤組成物とを用いて
同様に試験を行つた。試験結果を次表に示す。
FIELD OF THE INVENTION The present invention relates to bottle assemblies in which a polyethylene bottom lid is joined to a blow molded polyethylene terephthalate (PET) bottle by a novel hot melt adhesive composition. More particularly, the present invention relates to novel hot melt adhesive compositions having improved properties that are particularly useful in joining and assembling bottoms to PET bottles. BRIEF DESCRIPTION OF THE PRIOR ART Polyester bottles are widely used in the soft drink industry. These bottles are usually blow-molded, round-bottomed bottles that require a separate bottom lid to stand up straight. The bottom lid serves to keep the bottle sufficiently intact to withstand bottling, handling and storage conditions. The bottom lid is usually made of high-density polyethylene (HDPE) and is bonded to the bottle with hot melt adhesive. The forces that assembled bottles are subjected to during bottling, handling, and storage place the adhesive bond holding the bottom lid to the bottle under significant stress, which can cause the bottom lid and assembled bottle to peel or separate. Cause. Such stresses can cause empty bottles to delaminate before filling, so such bottles cannot be used in automatic filling lines. Once the bottle is filled, the pressure from the contents improves the mechanical fit between the bottle and the lid, causing the lid to remain attached to the bottle. However, once any part of the contents is lost, this improved fit is lost and the adhesive must prevent the bottle and lid from coming apart. The adhesive must also withstand the stresses to which the assembled bottle is subjected before and after filling due to varying temperature and humidity conditions. The soft drink filling industry has developed a series of standards that assembled bottles must meet. For example, an assembled bottle is cooled to -17.8°C (0〓) when empty and 4.5°C (40〓) when dropped from a height of 1.83 m (6 feet) and filled.
Do not let go when dropped from a height of 1.83 meters. Taylor et al. disclose in U.S. Pat. No. 4,212,910 (corresponding to Japanese Patent Application Laid-open No. 154,235/1983) that the adhesive composition is a styrene-butadiene-styrene type or styrene-isoprene-styrene type block copolymer, A prefabricated bottle is described and claimed which is a mixture of a tackifying resin, a stabilizer and a wax or oil diluent. Although this composition is an improvement over previously used adhesives, it is not without drawbacks. For example, the bond strength of the adhesive composition at room temperature is lower than required, and the temperature stability of the composition leaves room for improvement. SUMMARY OF THE INVENTION It is a general object of the present invention to ensure that the adhesive bond between the PET bottle and the bottom lid withstands all the normal stresses that the assembled bottle would be subjected to.
The purpose is to manufacture PET prefabricated bottles. Yet another object of the present invention is to provide an adhesive composition that, when used in PET prefabricated bottles, produces an adhesive bond that meets the standards required by the bottling industry. The adhesive composition used in the present invention is selected from the following (1).
It is a mixture of the components of (5): (1) A-B-A type block copolymer in which A is a monovinyl aromatic hydrocarbon and B is a conjugated diene or a rubber monoolefin.
(a) and a teleblock copolymer (b) consisting of a molecule having at least three branches radially branching from a central segment, each branch having a polystyrene terminal block and a butadiene central segment; (2)
an ethylene-vinyl acetate copolymer; (3) at least one tackifying resin that serves to increase the adhesion of the mixture system; (4) at least one stabilizer; and (5)
At least one type of wax or oil-based diluent. The adhesive composition used in the present invention contains an ethylene-vinyl acetate copolymer as one of its basic components, as disclosed in the US patent of Taylor et al.
It is significantly different from the adhesive composition of No. 4212910. The inventors have discovered that the addition of an ethylene-vinyl acetate copolymer to the adhesive composition described in the Taylor et al. patent provides all the advantages of the Taylor et al. has been improved,
They also discovered that the stability at high temperatures is improved. The discovery that the addition of ethylene-vinyl acetate copolymers provides such benefits is surprising. This is because the patent specification of Taylor et al. states that the use of known hot melt adhesives based on ethylene-vinyl acetate copolymer (EVA) cannot meet the standards of the bottling industry in the case of PET prefabricated bottles. (Column 1, lines 52-56 and column 6, lines 6-32 of the patent specification). The patent specifications of Taylor et al.
It is clear that there is no suggestion to those skilled in the art that the addition of ethylene-vinyl acetate copolymer to the Taylor et al. adhesive compositions would result in any improvement in these compositions. Assembled bottles made using the adhesive composition of the present invention have a bond that combines excellent adhesion and flexibility at low, normal and high temperatures, as well as high bond strength. DESCRIPTION OF THE PREFERRED EMBODIMENTS The block copolymer component (1) of the hot melt adhesive used in the present invention may be one of two specific sets: (a) Each monomer part is arranged alternately so as to have a general structure of A-B-A, where A is an inelastic block consisting of a monovinyl aromatic hydrocarbon monomer part, and B is an elastomeric polymer block consisting of either a conjugated diene monomer or a mono-olefin, such that the total concentration of the A block is in the range of about 10-50% of the total weight of the polymer. Sulfur elastic block polymer. Among these polymers, styrene is commonly used as the monovinyl aromatic hydrocarbon monomer.
The most commonly used conjugated diene monomers are butadiene-1,3 and isoprene. Thus, for example, styrene-butadiene-styrene polymers are available from Shell Chemical Co. as "Kraton 1101" and "Kraton 1102."
1101, -1102).
In addition, styrene-isoprene-styrene polymers are "Kraton 1107" and "Kraton 84-0554".
It is sold under the trademark . Although ethylene butylene monomer is commonly used as the monoolefin, other monomer components may also be used. A styrene-ethylenebutylene-styrene copolymer suitable for use is commercially available from Schiel Chemical Company under the trademark "Krayton G". A preferred block copolymer for use in the compositions of this invention is Kraton 1102. (b) A teleblock copolymer having at least three branches radially branching from a central segment, each branch comprising a molecule having a polystyrene terminal block and a butadiene central segment.
This type of block copolymer may also be referred to as a branched, polymerized butadiene center block with a polystyrene end block at the end of each branch. In all cases the number of butadiene units must be greater than the number of styrene units. A typical teleblock copolymer is trademarked as SOLPRENE and is manufactured by Phillips Petroleum Company.
Company). Mixtures of any of the above block copolymers can of course also be used as the base component of the adhesive used in the PET assembly bottles of the present invention. The ethylene-vinyl acetate copolymer component (2) of the hot melt adhesive used in the present invention is well known in the art, particularly as a resin for mixing in hot melt coatings and adhesives. Several manufacturers produce this copolymer.
Du Pont's Plastic Products and Resins Division manufactures a number of products with different combinations of composition and viscosity under the general trademark "Elvax". Elvax resin is sold in "grades" based on vinyl acetate content. For example, 200-series resins contain approximately 28 percent vinyl acetate, 300-series 25 percent, and 400-series 18 percent vinyl acetate.
Contains % vinyl acetate. Within each of these series, the higher the grade number, the higher the intrinsic viscosity. For example, the intrinsic viscosity of Elvax 210 is 0.54, Elvax 260 is 0.94, and Elvax 260 is 0.94.
265 is 1.01. Among these resins, Elvax 210 with a melt index of 400 is particularly effective when used in the composition of the present invention. All grades of Elvax are stabilized with the addition of 50-1000 ppm of butylated hydroxytoluene to prevent viscosity changes during use. It is believed that the tackifying resin (3) used in the hot melt adhesive of the present invention increases the adhesion of the block polymer. The term "tackifier resin" as used herein means the following resins (a) to (e). (a) natural and modified rosins such as rubber rosin, wood rosin, tall oil rosin, distilled rosin, hydrogenated rosin, dimerized rosin and polymerized rosin; (b) glycerin ester of pale rosin, hydrogenated rosin; (c) ASTM
A polyterpene resin with a softening point of approximately 60 to 140°C as measured by method E2858T. These high softening point polyterpene resins are usually obtained by polymerizing terpene hydrocarbons, such as the bicyclic monoterpene known as pinene, in the presence of Friedel-Crafts catalysts at relatively low temperatures; (d) (e) a phenol-modified terpene resin, such as a resin product obtained by condensing a bicyclic terpene and a phenol in an acidic medium; and (e) a ring and ball softening point of about 60 to 140°C.
Aliphatic petroleum-based hydrocarbon resins, among which resins with high softening points, are obtained by polymerization of monomers mainly consisting of olefins and diolefins. Particularly recommended is Sylvachem Corporation of Jacksonville.
It is a polymerized tall oil rosin sold under the name SYLVATAC95 from Jacksonville, Florida, Florida. The stabilizer (4) used in the hot melt adhesive compositions of the present invention, in some sense, stabilizes the susceptible block polymer and thus the entire adhesive system during the manufacture and use of the adhesive and further stabilizes the final bond. Helps protect against thermal and oxidative degradation commonly encountered in conditions to which the product is normally exposed. Ethylene-vinyl acetate copolymers are also believed to help protect the block polymer from thermal and oxidative degradation. Such degradation is usually manifested in a deterioration in appearance, physical properties, and practical performance. Stabilizers used include polyfunctional phenols such as high molecular weight sterically strained phenols and phenols containing sulfur and phosphorus. Hindered phenols are well known to those skilled in the art and are phenolic compounds characterized by having a sterically bulky group in the immediate vicinity of their phenolic hydroxyl group. In particular, at least one of the ortho positions of the phenolic hydroxyl group usually contains a tert-butyl group as a substituent. When such a sterically bulky substituent exists near a hydroxyl group, its stretching vibration and therefore its reactivity are suppressed. This steric hindrance thus provides a phenolic compound with stabilizing properties. Representative hindered phenols are 1,3,5-trimethyl-2,4,6-tris(3,5-di-tert-butyl-4-hydroxybenzyl)benzene, pentaerythrityltetrakis-3(3,5-di tert-butyl-4-hydroxyphenyl) propionate,
n-octadecyl-3(3,5-di-tert-butyl-
4-hydroxyphenyl)propionate; 4,
4'-methylene-bis(2,6-di-tert-butylphenol);2,2'-methylenebis(4-methyl-
6-tert-butylphenol);4,4'-thiobis(6-tert-butyl-o-cresol);2,6-di-tert-butylphenol); 6-(4-hydroxyphenoxy)-2, 4-bis(n-octylthio)-
1,3,5-triazine; 2,4,6-tris(4-hydroxy-3,5-di-tert-butylphenoxy)-1,3,5-triazine; di-n-octadecyl-3,5-di- tert-butyl-4-hydroxybenzylphosphonate; 2-(n-octylthio)ethyl-3,5-di-tert-butyl-4-hydroxybenzoate; and sorbitol hexa[3-(3,5-di-tert-butyl-4 -hydroxyphenyl)propionate]. A particularly recommended stabilizer is Tris (monophenyl phosphate), commercially available from Weston under the trade name TNPP. The performance of these stabilizers is further enhanced when combined with (1) and (2): (1) synergists, such as thiodipropionates and phosphites, and (2) acetic acid,
its salts, and chelating agents and metal deactivators such as disalicilal propylene diimine. Wax or oil-based diluent used in the present invention
(5) reduces the melt viscosity or cohesiveness of a hot melt adhesive composition without appreciably degrading its adhesive bonding properties. The wax-based diluent used includes the following: (1) Hardness measured by ASTM method D-1321 is about 0.1 to
120, the ASTM softening point is approximately 65.6~121℃ (150~
250〓) with a low molecular weight, for example 1000 ~
6000 polyethylene, (2) melting point about 54.5-79.5℃
(130~175〓) paraffin wax and ASTM
Melting point measured by method D127-60 is approximately 57.2-93.3℃
(135-200〓); (3) atactic polypropylene with a ring and ball softening point of approximately 120-160°C; and (4) Fischer-Tropsch wax. A synthetic wax made by polymerizing carbon monoxide and hydrogen. All of these wax-based diluents are solid at room temperature. Hydrogenated animal, fish, and vegetable oils such as hydrogenated tallow, pork oil, soybean oil, cottonseed oil, castor oil, menhedeine oil, and cod liver oil are solid at room temperature due to hydrogenation, so they cannot be used as wax-based diluents. It turned out to be useful as an equivalent item. These hydrides are often referred to in the adhesive industry as "animal or vegetable waxes." Additionally, hydrocarbon oils, especially naphthenic or paraffinic process oils, are also used as diluents in the present invention. In particular, paraffin wax with a melting point of 150℃ and white mineral oil
It is best to use it together with oil) USP. The novel hot melt adhesive composition of the present invention typically includes a block polymer at a concentration of about 20-40%, an ethylene-vinyl acetate copolymer at a concentration of about 5-20%, and a tackifier at a concentration of about 30-60%. Resin, concentration approximately 0.1-4%
stabilizers and a wax or oil concentration of about 10-30%. These concentrations are values calculated based on the total solid weight of the hot melt adhesive composition as 100%. The hot melt adhesive compositions used in the present invention are formulated using any technique known in the art. Typical methods are as follows:
A mixing device with a jacket, preferably of the Baker-Perkins type with an agitator.
Pour about half of the tackifying resin, all of the wax, oil, and stabilizer into a heavy-duty Perkins or Day-type mixer with a jacket, and immediately bring the temperature to about 121-176.7°C (250-350°C). ), preferably 149
Raise to ℃ (300〓). The exact temperature used will depend on the melting points of the particular ingredients. Once the starting mixture is melted and mixed, CO 2 is slowly bubbled through the mixture to cover the mixture before the block polymer is added. After this block polymer is dissolved, the ethylene-vinyl acetate copolymer is added and mixed until smooth.
Then add the remaining tackifying resin and continue mixing until well mixed. The viscosity of the hot melt composition is 162.8°C (325°C).
〓) is preferably about 4000 centipoise. Optional additives may be added to improve the properties of the hot melt composition. These additives include pigments such as titanium oxide and fillers such as talc and clay. The PET assembled bottle of the present invention is usually produced by feeding the bottle and the bottom lid onto a linear or centrifugal feeder, and applying hot melt adhesive in the form of small droplets from a multi-hole nozzle to a coating amount of about 0.4 to 0.75 g per bottom lid. The bottle and bottom lid are then squeezed together for at least 6.5 seconds to ensure that the droplets of hot melt adhesive are connected into a line and properly set. The assembled bottles are then labeled, packaged, and placed on pallets for shipping for bottling operations. The embodiments of the present invention will be explained in more detail with reference to the following reference examples and examples. Reference example: A sturdy pot-shaped mixer equipped with paddle-shaped stirring blades is heated to 149℃ (300℃), and the melting point is 65.6℃.
(150〓) Paraffin Wax 373.8 Kg (824 lb), White Mineral Oil USP 249 Kg (549 lb), Tris Monophenol Phosphate (Weston
TNPP) (Weston TMPP) 3.6Kg ((8 pounds)
and polymerized tall oil rosin (Silbatac 95
(Sylvatac95) 488.5Kg (1077lb) was loaded. The mixture was melted, mixed, and slowly charged with carbon dioxide, followed by the addition of 622.8 kg (1373 lbs.) of a block polymer available from Shell Chemical Company under the trademark "Kraton 1102."
After the block polymer had melted, 249 kg (549 lb) of ethylene-vinyl acetate copolymer (Elvax 210) having a melt index of 400 was added with stirring. After this mixture is smooth, polymerized tall oil rosin (Silbatac 95) 508Kg
(1120 lbs.) was added. When stirring is slowed down,
Continue mixing until you have a homogeneous, well-mixed mass. The molten mixture is poured into a partitioned container and allowed to solidify. The product thus obtained has a melt viscosity of 162.8 °C (325
〓) was about 4000 centipoise. Example Using the hot melt adhesive composition prepared in the reference example above, a PET prefabricated bottle was manufactured using conventional manufacturing equipment. This assembled bottle was tested using various test methods established by the bottling industry and was shown to meet or exceed these standards. For comparison, similar tests were conducted using the composition of the present invention and an adhesive composition that was identical to the composition of the present invention except that it did not contain the ethylene-vinyl acetate copolymer. The test results are shown in the table below.
【表】【table】
【表】【table】
【表】
上記の試験結果から、本発明で用いられるエチ
レン−酢酸ビニル共重合体含有接着剤は高温安定
性が非常に優れていること、低温から高温にわた
つて、特に高温においてPET/PE間に高度の接
着強さと極めて優れた耐熱クリープ性を与えるこ
と、そしてこれらを反映して本発明の組立てびん
は低温〜高温において応力下での接着剥れ、底ぶ
たの分離に極めてよく抗することが分る。
以上の実施例は具体的説明のためのものであ
り、本発明の範囲から逸脱することなしにその割
合、方法及び原材料を変えられることは当該技術
分野での習熟者には明らかである。それ故、本発
明は前記特許請求の範囲による以外は限定される
ものでない。[Table] From the above test results, it is clear that the adhesive containing ethylene-vinyl acetate copolymer used in the present invention has excellent high-temperature stability. The prefabricated bottle of the present invention is highly resistant to adhesive peeling and separation of the bottom lid under stress at low to high temperatures. I understand. It will be apparent to those skilled in the art that the above examples are illustrative and that the proportions, methods and materials may be varied without departing from the scope of the invention. Accordingly, the invention is not to be limited except as by the appended claims.
Claims (1)
(PET)びんと高密度ポリエチレン底ぶたを、A
がモノビニル芳香族炭化水素であり、Bが共役ジ
エンまたはゴム系モノオレフインのいずれかであ
るA−B−A型ブロツク共重合体(a)、および中心
セグメントから放射状に枝分れした少なくとも三
つの枝を持ち、その各枝がポリスチレンの末端ブ
ロツクとブタジエンの中心セグメントを持つ分子
から成るテレブロツク共重合体(b)から成る組から
選ばれた一種のブロツク共重合体(1)、エチレン−
酢酸ビニル共重合体(2)、系の接着性を増加させる
のに役立つ粘着付与樹脂(3)、安定剤(4)、及びワツ
クスまたは油系希釈剤(5)の混合物から成るホツト
メルト接着剤で結合させて成ることを特徴とする
ポリエチレンテレフタレート(PET)組立てび
ん。 2 ブロツク共重合体が、スチレン−ブタジエン
−スチレン−ブロツク共重合体であり、エチレン
−酢酸ビニル共重合体が約400のメルトインデツ
クスを持ち、約28%の酢酸ビニルを含む前記特許
請求の範囲第1項に記載のポリエチレンテレフタ
レート(PET)組立てびん。 3 ワツクス系希釈剤が硬度0.1〜120、ASTM
軟化点65.6〜121℃(150〜250〓)である低分子
量ポリエチレン、融点54.5〜79.5℃(130〜175
〓)の石油系ワツクス、融点57.2〜93.3℃(135
〜200〓)のミクロ結晶性ワツクス、環球式軟化
点120〜160℃のアタクチツクポリプロピレン、一
酸化炭素と水素との重合によつて造られた合成ワ
ツクス及び水素化−動物、−魚及び−植物油脂類
から成る群から選ばれる前記特許請求の範囲第1
項に記載のポリエチレンテレフタレート(PET)
組立てびん。 4 油系希釈剤が鉱油である前記特許請求の範囲
第1項に記載のポリエチレンテレフタレート
(PET)組立てびん。 5 ブロツク共重合体がスチレン−イソプレン−
スチレン−ブロツク共重合体である前記特許請求
の範囲第1項に記載のポリエチレンテレフタレー
ト(PET)組立てびん。 6 粘着付与樹脂が天然及び変性ロジン、天然及
び変性ロジンのグリセリン及びペンタエリトリト
ールエステル、軟化点60〜140℃のポリテルペン
樹脂、フエノール変性テルペン樹脂、及び環球式
軟化点が60〜140℃である脂肪族石油系炭化水素
樹脂から成る群から選ばれる前記特許請求の範囲
第1項に記載のポリエチレンテレフタレート
(PET)組立てびん。 7 安定剤が分子量の大きい立体障害フエノール
または多官能性フエノールである前記特許請求の
範囲第1項に記載のポリエチレンテレフタレート
(PET)組立てびん。 8 ホツトメルト接着剤が、その全固形分重量を
100%とした時、約20〜40%のブロツク重合体、
約5〜20%のエチレン−酢酸ビニル共重合体、約
30〜60%の粘着付与樹脂、約0.1〜4%の安定剤
及び10〜30%のワツクスまたは油系希釈剤を含む
前記特許請求の範囲第1項に記載のポリエチレン
テレフタレート(PET)組立てびん。[Claims] 1. A blow-molded polyethylene terephthalate (PET) bottle and a high-density polyethylene bottom lid,
is a monovinyl aromatic hydrocarbon, B is either a conjugated diene or a rubber monoolefin, and at least three copolymers branched radially from the central segment. A type of block copolymer (1) selected from the group consisting of teleblock copolymers (b) consisting of a molecule having branches, each branch having a terminal block of polystyrene and a central segment of butadiene, ethylene-
A hot melt adhesive consisting of a mixture of a vinyl acetate copolymer (2), a tackifying resin (3) that serves to increase the adhesion of the system, a stabilizer (4), and a wax or oil-based diluent (5). A polyethylene terephthalate (PET) assembled bottle characterized by being made by combining them. 2. The block copolymer is a styrene-butadiene-styrene block copolymer, and the ethylene-vinyl acetate copolymer has a melt index of about 400 and contains about 28% vinyl acetate. The polyethylene terephthalate (PET) assembled bottle described in paragraph 1. 3 Wax-based diluent has a hardness of 0.1 to 120, ASTM
Low molecular weight polyethylene with a softening point of 65.6~121℃ (150~250〓), a melting point of 54.5~79.5℃ (130~175〓)
〓) Petroleum-based wax, melting point 57.2-93.3℃ (135
Microcrystalline waxes of ~200㎓), atactic polypropylenes with a ring and ball softening point of 120-160°C, synthetic waxes made by polymerization of carbon monoxide and hydrogen, and hydrogenated animals, fish and plants. Claim 1 selected from the group consisting of oils and fats.
Polyethylene terephthalate (PET) as described in
Assembled bottle. 4. The polyethylene terephthalate (PET) prefabricated bottle according to claim 1, wherein the oil-based diluent is mineral oil. 5 The block copolymer is styrene-isoprene-
A polyethylene terephthalate (PET) assembly bottle according to claim 1, which is a styrene-block copolymer. 6 Tackifying resins include natural and modified rosins, glycerin and pentaerythritol esters of natural and modified rosins, polyterpene resins with a softening point of 60 to 140°C, phenol-modified terpene resins, and aliphatic resins with a ring and ball softening point of 60 to 140°C. A polyethylene terephthalate (PET) prefabricated bottle according to claim 1 selected from the group consisting of petroleum-based hydrocarbon resins. 7. The polyethylene terephthalate (PET) assembled bottle according to claim 1, wherein the stabilizer is a sterically hindered phenol or a polyfunctional phenol with a large molecular weight. 8 The total solids weight of a hot melt adhesive is
When taken as 100%, about 20 to 40% block polymer,
Approximately 5-20% ethylene-vinyl acetate copolymer, approx.
A polyethylene terephthalate (PET) prefabricated bottle according to claim 1, comprising 30-60% tackifying resin, about 0.1-4% stabilizer and 10-30% wax or oil diluent.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US06/367,738 US4394915A (en) | 1982-04-12 | 1982-04-12 | Hot melt adhesive compositions and bottle assemblies using said compositions |
US367738 | 1982-04-12 |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS58183773A JPS58183773A (en) | 1983-10-27 |
JPS6330215B2 true JPS6330215B2 (en) | 1988-06-16 |
Family
ID=23448404
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP57234864A Granted JPS58183773A (en) | 1982-04-12 | 1982-12-24 | Novel hot melt adhesive composition and sectional bottle |
Country Status (2)
Country | Link |
---|---|
US (1) | US4394915A (en) |
JP (1) | JPS58183773A (en) |
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FR2830257B1 (en) * | 2001-10-02 | 2006-12-01 | Bostik Findley | METHOD FOR COLLABLY ASSEMBLING HYDROPHOBIC AND OLEOPHOBIC SUBSTRATES FOR PACKAGING |
US6890982B2 (en) * | 2002-06-11 | 2005-05-10 | Marcus Oil And Chemical-Corp. | Wax for hot melt adhesive applications |
JP2005099712A (en) * | 2003-08-28 | 2005-04-14 | Sharp Corp | Driving circuit of display device, and display device |
US20060135694A1 (en) * | 2004-12-17 | 2006-06-22 | Vaughan Steven R | Hot melt adhesive composition |
DE102006054196A1 (en) * | 2006-11-15 | 2008-05-21 | Henkel Kgaa | Hot melt adhesives with improved adhesion |
SG188465A1 (en) | 2010-10-15 | 2013-05-31 | Exxonmobil Chem Patents Inc | Polypropylene-based adhesive compositions |
EP3328934A4 (en) * | 2015-10-30 | 2019-02-27 | Henkel AG & Co. KGaA | Damping hot melt composition |
EP3635067B1 (en) | 2017-05-22 | 2023-12-06 | H. B. Fuller Company | Hot melt adhesive composition |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5138549A (en) * | 1974-07-31 | 1976-03-31 | Heathcoat & Co Ltd | |
JPS5510437A (en) * | 1978-07-05 | 1980-01-24 | Nec Corp | Glass plate cutting method |
JPS55154235A (en) * | 1979-04-30 | 1980-12-01 | Nat Starch Chem Corp | Combined bottle made of polyester and terephthalate |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3749630A (en) * | 1971-06-25 | 1973-07-31 | Owens Illinois Inc | Process for bonding a glass container to a cup-shaped fitment with hot melt adhesive |
US3952898A (en) * | 1971-06-25 | 1976-04-27 | Owens-Illinois, Inc. | Preparation of crystalline hot melt composition |
DE3066399D1 (en) * | 1979-08-31 | 1984-03-08 | Dsm Resins Bv | Production of resins based on alpha-methyl styrene, styrene and a phenol as constituents, and their use in adhesives |
GB2066270B (en) * | 1979-12-26 | 1983-08-03 | Asahi Chemical Ind | Hot-melt pressure-sensitive adhesive composition |
-
1982
- 1982-04-12 US US06/367,738 patent/US4394915A/en not_active Expired - Lifetime
- 1982-12-24 JP JP57234864A patent/JPS58183773A/en active Granted
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5138549A (en) * | 1974-07-31 | 1976-03-31 | Heathcoat & Co Ltd | |
JPS5510437A (en) * | 1978-07-05 | 1980-01-24 | Nec Corp | Glass plate cutting method |
JPS55154235A (en) * | 1979-04-30 | 1980-12-01 | Nat Starch Chem Corp | Combined bottle made of polyester and terephthalate |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2004512421A (en) * | 2000-10-20 | 2004-04-22 | スリーエム イノベイティブ プロパティズ カンパニー | Thermoplastic additives for hot melt adhesives based on non-thermoplastic hydrocarbon elastomers |
Also Published As
Publication number | Publication date |
---|---|
US4394915A (en) | 1983-07-26 |
JPS58183773A (en) | 1983-10-27 |
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